Using colloidal silica as a zonal isolation material and fast path blocker in geological formations

ABSTRACT

A system for blocking fast flow paths in geological formations includes preparing a solution of colloidal silica having a nonviscous phase and a solid gel phase. The solution of colloidal silica is injected into the geological formations while the solution of colloidal silica is in the nonviscous phase. The solution of colloidal silica is directed into the fast flow paths and reaches the solid gel phase in the fast flow paths thereby blocking flow of fluid in the fast paths.

CROSS-REFERENCE TO RELATED APPLICATIONS

The present application is a Division of application Ser. No. 13/722,843filed Dec. 20, 2012, the disclosure of which is hereby incorporated byreference in its entirety for all purposes.

STATEMENT AS TO RIGHTS TO INVENTIONS MADE UNDER FEDERALLY SPONSOREDRESEARCH AND DEVELOPMENT

The United States Government has rights in this invention pursuant toContract No. DE-AC52-07NA27344 between the United States Department ofEnergy and Lawrence Livermore National Security, LLC for the operationof Lawrence Livermore National Laboratory.

BACKGROUND Field of Endeavor

The present invention relates to geological formations and moreparticularly to using colloidal silica to block fast flow paths and as azonal isolation material in geological formations.

State of Technology

U.S. Pat. No. 4,732,213 for colloidal silica-based fluid diversionprovides the state of technology information reproduced below. U.S. Pat.No. 4,732,213 is incorporated into this application in its entirety forall purposes by this reference.

A process for selectively plugging permeable zones in subterraneanformations or for plugging subterranean leaks which comprises injectinginto the permeable zone or the site of the subterranean leak an aqueoussolution containing 1 to 70 weight percent of a non-aggregated colloidalsilica sol having a particle size in the range between 4 and 100 nm anda pH in the range between about 1 and 10, and causing said solution togel in said zone or at said site.

Recovery of oil from subterranean formations frequently involvesdisplacing crude oil with a driving fluid, e.g., gas, water, brine,steam, polymer solution, foam, or micellar solution. Ideally, suchtechniques (commonly called flooding techniques) would provide a bank ofoil of substantial depth being driven to a producing well; in practice,that frequently is not the case. Oil-bearing strata are usuallyheterogeneous, some parts of them being more permeable to a drivingfluid than others. As a consequence, channeling frequently occurs sothat the driving fluid flows preferentially through zones depleted ofoil (so-called “thief” zones) rather than through those parts of thestrata which contain sufficient oil to make oil-recovery operationsprofitable. High permeability zones can also cause undesirable loss ofdrilling fluids when a well (e.g., water, oil or waste disposal) isbeing drilled. Misplaced casing perforations or casing leaks are anothercause of channeling of the driving fluid through zones of highpermeability in the subterranean formations. In addition, casing leakssometimes occur in the annular region above the injection or productionpacker, and need to be dealt with whether the leaks occur in high or lowpermeability zones.

A variety of fluid diversion techniques have been proposed in the priorart. Typically, a gel is formed in situ in zones of very highpermeability, thus plugging them and causing fluid to flow through zoneswhich originally were of lower permeability than those which have beenplugged. However, such techniques are in general not suitable attemperatures in excess of about 100° C. and are limited to short geltimes, e.g., less than 12 hours, thereby severely limiting theireffectiveness. Thus, the prior art fluid diversion gels cannot be usedin high temperature reservoirs commonly encountered in deep wells or insteam-flood operations, and in many cases the treatment composition canbe pumped only a short distance from the wellbore before it gelsregardless of reservoir temperature.

U.S. Published Patent Application No. 2009/0260544 for well treatmentcompositions and methods utilizing nano-particles provides the state oftechnology information reproduced below. U.S. Published PatentApplication No. 2009/0260544 is incorporated into this into thisapplication in its entirety for all purposes by this reference.

An exemplary embodiment of the present invention provides a method ofcementing. The method comprises introducing a cement composition into asubterranean formation, wherein the cement composition comprises cement,water and at least one nano-particle selected from the group consistingof particulate nano-silica, nano-alumina, nano-zinc oxide, nano-boron,nano-iron oxide and combinations thereof.

Another exemplary embodiment of the present invention provides a methodof cementing in a subterranean formation. The method comprises includingencapsulated nano-particles in a cement composition. The method furthercomprises introducing the cement composition into the subterraneanformation.

Another exemplary embodiment of the present invention provides a methodof accelerating set time of a cement composition. The method comprisesincluding particulate nano-silica in a cement composition. The methodfurther comprises introducing the cement composition into a subterraneanformation. The method further comprises allowing the cement compositionto set in the subterranean formation.

Another exemplary embodiment of the present invention provides a wellcement composition. The well cement composition comprises cement waterand at least one nano-particle selected from the group consisting ofparticulate nano-silica, nano-alumina, nano-zinc oxide, nano-boron,nano-iron oxide and combinations thereof.

Another exemplary embodiment of the present invention provides a methodof treating a subterranean formation. The method includes introducing atreatment fluid into a subterranean formation, wherein the treatmentfluid comprises at least one nano-particle selected from the groupconsisting of particulate nano-silica, nano-alumina, nano-zinc oxide,nano-boron, nano-iron oxide, and combinations thereof.

Another exemplary embodiment of the present invention provides a methodof using nano-particles in a well treatment fluid. The method comprisesincluding encapsulated nano-particles in the well treatment fluid.

Another exemplary embodiment of the present invention provides a welltreatment fluid. An embodiment of the well treatment fluid comprises atleast one nano-particle selected from the group consisting ofparticulate nano-silica, nano-alumina, nano-zinc oxide, nano-boron,nano-iron oxide, and combinations thereof. Another embodiment of thewell treatment fluid comprises encapsulated nano-particles.

U.S. Published Patent Application No. 2009/0081105 for silica extractionfrom geothermal water provides the state of technology informationreproduced below. U.S. Published Patent Application No. 2009/0081105 isincorporated into this application in its entirety for all purposes bythis reference.

Geothermal fluids are produced from subsurface reservoirs at depthscommonly between 500 and 3000 meters. Their heat is extracted and usedto generate power. The fluids are then reinjected into the subsurface toreplenish the fluid reservoir. Resource removal optimally takes placeafter or near the end of the energy extraction process, but prior toreinjection. The temperatures of reinjected fluids are commonly between50 and 150° C. and pressures at or slightly above steam saturation. Insome cases, mineral extraction may allow further energy extraction that,without treatment, would be uneconomic due to scale formation. Forexample, the geothermal plants at Wairakei, New Zealand terminate energyextraction as the fluids cool to below 130° C. because silica scalingbecomes too difficult to control (Brown, 2000, Proc. World GeothermalCongress p. 533). Silica extraction will allow additional energyextraction to lower temperatures. Mineral recovery also improves theeconomics of geothermal energy production by helping to minimize scalingboth in the plant and in reinjection wells.

Many constituents of geothermal fluids have value provided they can beseparated and purified. Previous published work on extraction ofresources from geothermal fluids has focused on a wide variety ofmaterials including precious and platinum group metals, zinc, lead,copper, manganese, rare earths, silica, lithium, arsenic, antimony,boron, bromine, iodine, strontium and barium sulfate, precipitatedcalcium carbonate, calcium chloride, potash, table salt, and sodiumsulfate. Most of this work has focused on extraction of silica, lithium,and zinc. Typical recovery methods include acid leaching, biochemicalleaching, evaporation and precipitation as sulfides.

Silica is an ubiquitous component of geothermal fluids and must beremoved or reduced in concentration to allow other components to beremoved. Most hydrothermal systems equilibrate with quartz (SiO.sub.2)causing the fluids to have silica concentrations that reflect thetemperature of the reservoir—the hotter the reservoir, the higher thesilica concentration of the fluid.

During energy production, the geothermal fluid cools and some water isextracted as steam. Both processes cause the silica to becomeincreasingly supersaturated. Eventually the silica tends to precipitateand form scale on various plant components or in reinjection wells.Silica will also tend to precipitate on mineral extraction processingequipment if not removed prior to mineral co-production. Thus a key needfor mineral co-production is the elimination of silica scaling.

SUMMARY

Features and advantages of the present invention will become apparentfrom the following description. Applicants are providing thisdescription, which includes drawings and examples of specificembodiments, to give a broad representation of the invention. Variouschanges and modifications within the spirit and scope of the inventionwill become apparent to those skilled in the art from this descriptionand by practice of the invention. The scope of the invention is notintended to be limited to the particular forms disclosed and theinvention covers all modifications, equivalents, and alternativesfalling within the spirit and scope of the invention as defined by theclaims.

The present invention provides a system for blocking fast flow paths ingeological formations or in other ways causing beneficial alteration oftheir permeability and flow properties. The system includes preparing asolution of colloidal silica having a nonviscous phase and a solid gelphase. The solution of colloidal silica is injected into the geologicalformations while the solution of colloidal silica is in the nonviscousphase. The solution of colloidal silica is directed into the fast flowpaths and transforms into the solid gel phase in the fast flow pathsthereby blocking flow of fluid in the fast paths. Current methods ofattempting to block fast flow paths include the use of common Portlandcements, polymers, and carbonate minerals to cement or block the fastflow paths.

The present invention has use in enhancing geothermal systems. Thepresent invention has use in enhanced geothermal systems wherehydrofracing has introduced unwanted fast paths. The present inventionalso has use in blocking fast paths in operations to recover oil andnatural gas. The present invention has use in blocking fast paths inoperations to recover oil and natural gas after hydrofracing. Thepresent invention has use in blocking fast paths in operations torecover oil and natural gas after hydrofracing in enhanced oil recovery.The present invention has use in blocking fast paths in operations torecover oil and natural gas after hydrofracing in tight shale gasformations. The present invention has use in blocking of fast paths insite remediation operations such as those to block leakage ofcontaminants from underground tanks or from leaking surface wasteinstallations, such as radioactive waste storage facilities. The presentinvention has use in carbon dioxide sequestering by blocking flow pathsin cap rock or other geological formations. The present invention hasuse in prevention of leakage of drilling and production fluids aroundsubsurface well bores. The present invention has use in modification ofgeothermal reservoir properties such that they are able to producegreater amounts of energy. The present invention has use in lowering theamount of water loss from a geothermal field by emplacement in theperimeter of the geothermal field such that it acts as an impermeablebarrier surrounding the active reservoir.

Blocking Fast Paths in Geothermal Formations

In one embodiment, the present invention provides a system whereincolloidal silica harvested from geothermal fluids is used topreferentially block fast paths in the subsurface allowing greaterenergy production from geothermal power plants. The silica is harvestedusing existing silica extraction technologies and concentrated insolution such that it will transform, after some incubation time, into asolid gel. In one embodiment of the present invention, the solution isreinjected into the subsurface while non-viscous and flows to thepermeable (fast-path) zone, but then transforms to a gel in that zoneand acts to block further fluid transport in that zone. The length ofthe incubation period is adjusted by adjusting the silica content,colloid size, salinity, and pH, or predetermined combinations of silicacontent, colloid size, salinity, and pH, to achieve the desiredtransport time and positioning of the solid gel. The results ofreservoir modeling and tracer test results are used to guide theemplacement process in order to locate the silica gel in the desiredlocation.

Blocking Fast Paths in Oil and Gas Formations

In one embodiment a solution of colloidal silica is prepared having anonviscous phase with a predetermined incubation period before forming asolid gel. The predetermined incubation period is established byadjusting the silica content, colloid size, salinity, and pH, orpredetermined combinations of silica content, colloid size, salinity,and pH. In one embodiment the system includes reservoir modeling in thestep of allowing the solution of colloidal silica to flow into the fastpaths and reach the solid gel phase thereby blocking the flow of theproduction fluid in the fast paths and diverting the flow of theproduction fluid into the other paths.

Blocking Fast Paths in Environmentally Contaminated Formations

The present invention has use in blocking of fast paths in siteremediation operations such as those to block leakage of contaminantsfrom underground tanks, isolate subsurface contaminant sources, or fromleaking surface waste installations, such as radioactive waste storagefacilities.

Blocking Fast Paths in Carbon Dioxide Sequestering Formations

The present invention has use in carbon dioxide sequestering by blockingflow paths in cap rock or other geological formations.

The invention is susceptible to modifications and alternative forms.Specific embodiments are shown by way of example. It is to be understoodthat the invention is not limited to the particular forms disclosed. Theinvention covers all modifications, equivalents, and alternativesfalling within the spirit and scope of the invention as defined by theclaims.

BRIEF DESCRIPTION OF THE DRAWINGS

The accompanying drawings, which are incorporated into and constitute apart of the specification, illustrate specific embodiments of theinvention and, together with the general description of the inventiongiven above, and the detailed description of the specific embodiments,serve to explain the principles of the invention.

FIG. 1 is an illustration of a geothermal system incorporating thepresent invention.

FIG. 2 show a section of the FIG. 1 fractured geothermal formation ingreater detail.

FIG. 3 illustrates one example of a system of the present invention.

FIG. 4 illustrates cryptocrystalline silica (agate) formed in thefractured geothermal formation.

FIG. 5 illustrates another example of a system of the present invention.

FIG. 6 illustrates cryptocrystalline silica (agate) formed in thefractured geothermal formation.

FIG. 7 is an illustration of a geothermal system incorporating anotherembodiment the present invention.

FIG. 8 illustrates a system with an oil reservoir having an injectionand a production well where enhanced oil recovery is taking place.

FIG. 9 shows sections of the petroleum reservoir including areas whereinjected fluids may travel.

FIG. 10 shows sections of the petroleum reservoir including areas whereinjected fluids may travel where enhanced oil recovery is taking place.

FIG. 11 illustrates another example of a system of the present inventionin connection with subsurface reservoir used for storage of carbondioxide.

FIG. 12 illustrates another example of a system of the present inventionto prevent leakage into or out of well.

FIG. 13 illustrates another example of a system of the present inventionto prevent leakage into or out of well.

FIG. 14 illustrates another example of a system of the present inventionin connection with leakage from an underground storage tank.

FIG. 15 illustrates another example of a system of the present inventionin connection with leakage from an underground storage tank.

FIG. 16 illustrates an example of a system of the present invention inconnection with cementing a pipe in a borehole in a formation.

DETAILED DESCRIPTION OF SPECIFIC EMBODIMENTS

Referring to the drawings, to the following detailed description, and toincorporated materials, detailed information about the invention isprovided including the description of specific embodiments. The detaileddescription serves to explain the principles of the invention. Theinvention is susceptible to modifications and alternative forms. Theinvention is not limited to the particular forms disclosed. Theinvention covers all modifications, equivalents, and alternativesfalling within the spirit and scope of the invention as defined by theclaims.

Referring now to the drawings and in particular to FIG. 1, a geothermalsystem incorporating the present invention is illustrated. Thegeothermal system is designated generally by the reference numeral 100.The geothermal system 100 includes a first well 104 designated as aninjection well and a second well 106 designated as extraction orproduction well. The first well 104 (injection well) and the second well106 (extraction well) are shown extending into a geothermal formation102. Fluid is injected into the first well 104 (injection well) and thefluid is extracted at the second well 106 (extraction well). The fluidfrom the second well flows into the power generation/cooling system 108.

A section of the fractured geothermal formation within the dotted circlein FIG. 1 is designated by the reference numeral 110. This section ofthe fractured geothermal formation 110 within the dotted circle is madeup of fractured rock 110. The fluid from the injection well 104 iscirculated through the fractured rock 110 where it is heated by thegeothermal formation 110. This circulation pattern illustrates basicfeatures of the production of energy from the geothermal formation 102.Hot dry rock resources occur at depths of 3 to 5 miles everywherebeneath the Earth's surface and at lesser depths in certain areas.Access to these resources involves injecting water down the first well104, circulating the water through the hot fractured rock 110, anddrawing off the heated water from the second well 106. A major drawbackfor current attempts to engineer geothermal systems is the existence of‘fast paths’—high permeability zones that short-circuit flow and allowrapid movement of fluid from the first well 104, the injection well, tothe second well 206, the production well. The fluid is not able toacquire much heat during its reduced contact time, and the fieldproduces less energy.

Referring now to FIG. 2 the section 110 of the fractured geothermalformation within the dotted circle is shown in greater detail. Hot dryrock resources in the form of heated formations occur at depths of 3 to5 miles everywhere beneath the Earth's surface and at lesser depths incertain areas. Access to these resources involves injecting water downthe first well 104, circulating the water through the hot fractured rock110, and drawing off the heated water from the second well 106. A majordrawback for current attempts to engineer geothermal systems is theexistence of “fast paths” that are high permeability zones thatshort-circuit flow and allow rapid movement of fluid from the first well104, the injection well, to the second well 106, the production well.The fluid is not able to acquire much heat during its reduced contacttime, and the field produces less energy.

As shown in FIG. 2, the section 110 of the fractured geothermalformation includes the “fast paths” permeability zones designate by thereference numeral 1114 which allow rapid movement of the fluid asillustrated by the arrows 112. The fractured geothermal formation alsoincludes the smaller permeability zones designate by the referencenumeral 1116 which provide a much slower movement of the fluid asillustrated by the arrows 116 a. The “fast paths” 114 allow rapidmovement of fluid through the section 110 of the fractured geothermalformation and short-circuit flow preventing or reducing flow through thesmaller permeability zones 116. The fluid is not able to acquire muchheat during its reduced contact time, and the field produces lessenergy.

The present invention provides a system that uses colloidal silica as acementing agent to preferentially reduce permeability in “fast pathzones” in a geothermal formation. Colloidal silica solutions are “tuned”in terms of silica concentration and solution composition so that thesilica solution transforms to a gel with the desired timing. Whereasfreshly-made colloidal silica solutions have viscosities only slightlygreater than water, over time the silica sols link forming a 3-D networkwhich gives rise to a large increase in viscosity. This transition togel follows an incubation period during which there is little change inviscosity. The gel is a material with properties similar to those of avery dense and viscous gelatin. Over long times, the gel willre-structure and dehydrate to form microcrystalline silica,mineralogically identical to natural vein-filling agate. Anyenvironmental effects of emplacement of this material is minimal.

The present invention will be further explained, illustrated, anddescribed in the following examples of systems of the present invention.The examples demonstrate the utility and/or function of the inventionand helps provide a full describe of the invention.

Example 1

Referring now to FIG. 3 one example of a system of the present inventionis illustrated and described. The section 110 of the fracturedgeothermal formation within the dotted circle is illustrated in detail.The section 110 of the fractured geothermal formation includes the “fastpaths” 114 permeability zones, which without the present invention,would allow rapid movement of the fluid through the geothermal formationand the fluid would not be able to acquire much heat during its reducedcontact time, and the field would produce less energy.

The present invention uses colloidal silica as a cementing agent topreferentially reduce permeability in the fast path zones 114 in thegeothermal formation 110. As illustrated in FIG. 3 colloidal silica 118is introduced into the fast path zones 114. A desired gelation time isselected with reservoir modeling and tracer test results to predicttransport times. By combining the two the process is tuned such thatgelation of the injected colloidal silica 118 happens in the fast pathzones 114, effectively blocking these zones 114 and forcing fluid flowthrough zones 116 that provide higher heat transfer. The rate at whichcolloidal silica solutions transform to gel is affected by the size andconcentration of silica colloids, the pH, the salt content of thecoexisting fluid, and the temperature. By adjusting one or more of theseparameters, the colloidal silica solutions that transform to gels areprovided on time scales varying from a few seconds to many days. Thepresent invention provides a desired gelation time, with reservoirmodeling to predict transport times. By combining the two the process istuned.

Referring now to FIG. 4, the colloidal silica has initially been used asa cementing agent to block the fast path zones 114 in the geothermalformation 110. Over longer time periods, the colloidal silica 118 willage and dehydrate to form cryptocrystalline silica (agate) 120, whichwill remain as a permanent feature of the geothermal reservoir. Thecolloidal silica was previously introduced into the fast path zones 114.This was accomplished using a desired gelation time that was selectedwith reservoir modeling to predict transport times. By combining the twothe process was tuned such that gelation of the injected colloidalsilica happened in the fast path zones 114, effectively blocking thesezones 114 and forcing fluid flow through zones 116 that provide higherheat transfer. The colloidal silica has aged and dehydrated to formcryptocrystalline silica (agate) 120. The cryptocrystalline silica(agate) 120 remains as a permanent feature of the geothermal formation110.

Example 2

Referring now to FIG. 5, another example of a system of the presentinvention is illustrated and described. The section 110 of the fracturedgeothermal formation within the dotted circle shown in FIG. 1 is shownin greater detail in FIG. 5. The section 110 of the fractured geothermalformation includes the “fast paths” permeability zones designate by thereference numeral 1114 which allow rapid movement of the fluid asillustrated by the arrows 112. The fractured geothermal formation alsoincludes the smaller permeability zones designate by the referencenumeral 116 which provide a much slower movement of the fluid asillustrated by the arrows 116 a. The “fast paths” 114 allow rapidmovement of fluid through the section 110 of the fractured geothermalformation and short-circuit flow preventing or reducing flow through thesmaller permeability zones 116. The fluid in the fast paths 114 is notable to acquire much heat during its reduced contact time, and the fieldproduces less energy.

The present invention uses colloidal silica 122 as a cementing agent topreferentially reduce permeability in the fast path zones 114 in thegeothermal formation 110. Colloidal silica 122 is introduced into thefast path zones 114. A desired gelation time is selected with reservoirmodeling to predict transport times. By combining the two the process istuned such that gelation of the injected colloidal silica 122 happens inthe fast path zones 114, effectively blocking these zones 114 andforcing fluid flow through zones 116 that provide higher heat transfer.The rate at which colloidal silica solutions transform to gel isaffected by the size and concentration of silica colloids, the pH, thesalt content of the coexisting fluid, and the temperature. By adjustingone or more of these parameters, the colloidal silica solutions thattransform to gels are provided on time scales varying from a few secondsto many days. The present invention provides a desired gelation time,with reservoir modeling to predict transport times. By combining the twothe process is tuned.

Example 3

Referring now to FIG. 7, a geothermal system incorporating anotherembodiment the present invention is illustrated. The geothermal systemis designated generally by the reference numeral 700. The geothermalsystem 700 includes a first well 704 designated as an injection well anda second well 706 designated as extraction or production well. The firstwell 704 (injection well) and the second well 706 (extraction well) areshown extending into a geothermal formation 702.

Fluid is injected into the first well 704 (injection well) and the fluidis extracted at the second well 706 (extraction well). The fluid fromthe second well flows into the power generation/cooling system 708. Thegeothermal formation 702 includes fractured geothermal formations madeup of fractured rock. The fluid from the injection well 704 iscirculated through the fractured rock 710 where it is heated by thegeothermal formation 710. This circulation pattern illustrates basicfeatures of the production of energy from the geothermal formation 702.(EGS) resources occur at depths of 3 to 5 miles everywhere beneath theEarth's surface and at lesser depths in certain areas. Access to theseresources involves injecting water down the first well 704, circulatingthe water through the hot fractured rock 710, and drawing off the heatedwater from the second well 706.

It is desirable to enhance production of geothermal energy from theformation 702 by reducing the flow of the fluid into formations otherthan the geothermal between the first well 704 (injection well) and thesecond well 706 (extraction well). This is accomplished by creatingreduced permeability sections zones 710 of the geothermal reservoirfield are areas where injected fluids may travel and because they arenot in the flow path between injection well and production well will benot be brought to the surface in the production well and will thereforenot provide geothermal energy. The fluids are lost from the system andas a consequence make it necessary to add additional water to theinjection well at some cost to the field operations.

As illustrated in FIG. 7, the reduced permeability sections 710 arelocated outside of the primary geothermal energy formation 702 betweenthe first well 704 (injection well) and the second well 706 (extractionwell). The present invention uses colloidal silica as a cementing agentto preferentially reduce permeability in these zones surrounding thetarget zone of energy production and prevent water loss into thesurrounding zones. This is illustrated by the arrows 710 a. A desiredgelation time is selected with reservoir modeling and tracer testresults such that gelation of the injected colloidal silica happens inthe permeable zones surrounding the geothermal reservoir. The emplacedgel blocks the flow of injected fluid away from the geothermal reservoirand in so doing increases the amount of energy that is available forproduction and lowers the amount of water lost from the system. The gelsmay be emplaced using the existing injection and production wells, Orother wells if they exist or new well if it is affordable DOES A PERIODBELONG HERE?????

The rate at which colloidal silica solutions transform to gel isaffected by the size and concentration of silica colloids, the pH, andsalt content of the fluids, and the temperature. By adjusting one ofmore of these parameters, the colloidal silica solutions transform togels on time scales of a few seconds to many days. The present inventionprovides a desired gelation time with reservoir modeling providing thetarget gelation time for emplacement at the desired location. Bycombining the two the process is tuned.

Example 4

Referring now to FIGS. 8, 9, and 10; a system incorporating anotherembodiment the present invention is illustrated. This embodiment of thepresent invention is a system with an oil reservoir 802 having aninjection 804 and a production well 806 where enhanced oil recovery istaking place. The system is designated generally by the referencenumeral 800. The system 800 includes a first well 804 designated as aninjection well and a second well 806 designated as extraction orproduction well. The first well 804 (injection well) and the second well806 (extraction well) are shown extending into the oil reservoir 802.Fluids are injected at 804 as illustrated by the arrows 804 a and oilextracted at 806 as illustrated by the arrows 806 a. The injected fluiddisplaces the existing subsurface fluid which contains some fraction ofpetroleum which is brought to the surface in the production well.

Referring now to FIGS. 9 and 10, sections 810 of the petroleum reservoirare shown where enhanced oil recovery is being implemented by thepresent invention. FIGS. 9 and 10 show sections 810 of the petroleumreservoir which are areas where injected fluids may travel and becausethey do not contain liquid petroleum, or because liquid petroleumpreviously present has already been removed, they do not contribute toproduction of petroleum from the production well 806 of FIG. 8. Flowpaths 814 and 816 of FIG. 9 contain deposits of liquid petroleum but thedeposits are not in the flow path and are not moved towards theproduction well between injection well and production well because theinjected fluid travels primarily through zone 812.

Referring to FIG. 10, the present invention uses colloidal silica as acementing agent to preferentially reduce permeability in zone 812 suchthat injected fluid is forced to travel through zones 814 and 816 and inso doing cause displacement of the liquid petroleum through thereservoir to the production well 806 of FIG. 8, where it is brought tothe surface. FIG. 10 illustrates that deposits 118 of liquid petroleumhave been moved into flow channel 812. The colloidal silica solution isinjected with known chemical properties such that it will transform to agel after a given amount of time when it is predicted to be present inthe fast path zone 812. Such predictions may be made using reservoirmodeling and using the results of tracer tests.

The rate at which colloidal silica solutions transform to gel isaffected by the size and concentration of silica colloids, the pH, andsalt content of the fluids, and the temperature. By adjusting one ofmore of these parameters, the colloidal silica solutions transform togels on time scales of a few seconds to many days. The present inventionprovides a desired gelation time with reservoir modeling providing thetarget gelation time for emplacement at the desired location. Bycombining the two the process is tuned.

Example 5

Another example of a system of the present invention is illustrated anddescribed in FIG. 11 which shows a subsurface reservoir used for storageof carbon dioxide. The system is designated generally by the referencenumeral 1100. As illustrated in FIG. 11, CO₂ is injected into thesubsurface in an injection well 1102 where it fills pore space withinthe rock. Because the CO₂ phase is less dense than aqueous brines thatco-exist in the subsurface, it will, over time, tend to rise vertically.The reservoir contains a layer 1106 (“cap rock”) that is impermeable toCO₂ migration and thus provides a barrier to upward migration of CO₂.Although formations are chosen such that they have cap rocks that arebelieved to be entirely impermeable to CO₂ escape, they may in fact havefractures or other permeable pathways that would allow CO₂ passage.

Referring to FIG. 11, the present invention uses colloidal silica 1110as a cementing agent to preferentially fill permeable pathways 1108 inthe cap rock 1106 and prevent CO₂ leakage. The colloidal silicasolutions are injected into the subsurface using the existing injectionwells for CO₂ emplacement, or injected using wells drilled for thepurpose of gel emplacement. The colloidal silica solutions are preparedsuch that they have densities lower than the brines contained in therocks beneath the cap rock. This is done by varying the silica contentof the fluids. In this way, the gel solutions will migrate upwards intothe cap rock where they will gel in the fracture zones and prevent CO₂leakage.

The colloidal silica solution is injected with known chemical propertiessuch that it will transform to a gel after a given amount of time whenit is predicted to be present in the fracture zones of the cap rock.Such predictions may be made using reservoir modeling and using theresults of tracer tests.

The rate at which colloidal silica solutions transform to gel isaffected by the size and concentration of silica colloids, the pH, andsalt content of the fluids, and the temperature. By adjusting one ofmore of these parameters, the colloidal silica solutions transform togels on time scales of a few seconds to many days. The present inventionprovides a desired gelation time with reservoir modeling providing thetarget gelation time for emplacement at the desired location. Bycombining the two the process is tuned.

Example 6

The Another example of a system of the present invention is illustratedand described in FIG. 12 which shows a well used for injection orproduction of subsurface fluids. The system is designated generally bythe reference numeral 1200. The subsurface fluids may contain brine,non-aqueous fluids, pressurized carbon dioxide, or other types offluids. Although measures are taken to prevent leakage into or out ofwell, such as metal casings used to line the wells and cements andgrouts used to fill any open space surrounding the well, wells commonlyleak and in so doing may cause unwanted contamination of surroundingfluids such as water aquifers used as public water supplies. Asillustrated in FIG. 12, well casing 1202 may corrode and cause leakage,cements may crack and allow fluid migration as illustrated by the arrow1204. In addition, commonly used cements and grouts are more viscousthan water and often do not impregnate the subsurface and block passagesthat are accessible to water, having a much lower viscosity.

Referring to FIG. 13, the present invention designated generally by thereference numeral 1300 uses colloidal silica 1302 as a cementing agentto preferentially fill all permeable pathways surrounding the well bore1304. The gel may be emplaced in the formation 1306 by pumping it downthrough the well to the bottom of the well where it then rises along theoutside of the well casing and fills all accessible pore space 1308. Thecolloidal silica solutions are prepared such that they have gelationtimes that allow the low viscosity fluid phase adequate time to reachall targeted zones surrounding the well bore. The solutions thentransform to a solid material that will help to prevent leakage into orout of the well bore and thus prevent unwanted fluids from contaminatingaquifers or other subsurface features that would be negatively impactedby fluid leakage from the well. Colloidal silica has an advantage overother commonly used cementing materials of having a very low(water-like) viscosity such that it will penetrate more deeply intoexisting fractures and pore spaces and block subsequent flow. Colloidalsilica is also unreactive in the subsurface and will not contaminate orreact with existing materials in unwanted or damaging ways. For exampleit will not over time decompose to give off toxic compounds such asmight be the case for polymeric cementing agents. Silica gel ages toform amorphous silica, a type of agate which is naturally abundant inthe subsurface. Conventional cements such as Portland Cements have veryhigh pH and may react in unwanted ways with existing fluids and rocks inthe subsurface.

The rate at which colloidal silica solutions transform to gel isaffected by the size and concentration of silica colloids, the pH, andsalt content of the fluids, and the temperature. By adjusting one ofmore of these parameters, the colloidal silica solutions transform togels on time scales of a few seconds to many days. The present inventionprovides a desired gelation time with reservoir modeling providing thetarget gelation time for emplacement at the desired location. Bycombining the two the process is tuned.

Example 7

Another example of a system of the present invention is illustrated anddescribed in FIGS. 14 and 15. This example is designated generally bythe reference numeral 1400. Referring to FIG. 14, an underground wastestorage tank 1402 which contains hazardous liquid waste 1404 isillustrated. The tank 1402 has corroded and is now leaking through leak1406 as illustrated by the arrows 1408. The hazardous materials 1404 areshown migrating into the subsurface formation 1410 where they migrateaway from the storage site and may cause contamination of local watersupplies or in other ways have a negative impact on the localenvironment.

Referring to FIG. 15, the present invention 1400 uses colloidal silica1500 as a cementing agent to preferentially block leakage 1406 ofcontaminants 1404 from the tank 1402. This is accomplished by pumping1502 the material 1500 through a well 1504 drilled so as to access thesubsurface in the vicinity of the leakage zones 1408. Colloidal silica1500 is pumped into the subsurface in the leakage zones 1408 and tunedsuch that after it reaches that zone in a low viscosity liquid statewill transform into an impermeable gel 1506 that blocks leakage from thetank.

The rate at which colloidal silica solutions transform to gel isaffected by the size and concentration of silica colloids, the pH, andsalt content of the fluids, and the temperature. By adjusting one ofmore of these parameters, the colloidal silica solutions transform togels on time scales of a few seconds to many days. The present inventionprovides a desired gelation time with reservoir modeling providing thetarget gelation time for emplacement at the desired location. Bycombining the two the process is tuned.

Example 8

Another example of a system of the present invention is illustrated anddescribed in FIG. 16 which shows a system of cementing a pipe in aborehole in a formation. The system is designated generally by thereference numeral 1600. The system 1600 provides application of a liquidslurry of colloidal silica to various points inside or outside a pipe1606 in a borehole 1602 in a formation 1604.

The system 1600 includes preparing a solution of colloidal silica 1616having a nonviscous phase and a solid gel phase and injecting thesolution of colloidal silica 1616 into the borehole 1602 while saidsolution of colloidal silica is in said nonviscous phase. The solutionof colloidal silica 1616 flows through pipe 1606 into the borehole 1602an up the annulus between the pipe 1606 and the wall 1608 of theborehole 1602. The colloidal silica 1616 is allowed to harden cementingthe pipe 1606 in the borehole 1602 in the formation 1604.

While the invention may be susceptible to various modifications andalternative forms, specific embodiments have been shown by way ofexample in the drawings and have been described in detail herein.However, it should be understood that the invention is not intended tobe limited to the particular forms disclosed. Rather, the invention isto cover all modifications, equivalents, and alternatives falling withinthe spirit and scope of the invention as defined by the followingappended claims.

The invention claimed is:
 1. A method of blocking flow in fast flowpaths in a geological formation, comprising the steps of: preparing asolution of colloidal silica having a nonviscous phase and a solid gelphase, injecting said solution of colloidal silica into the geologicalformation while said solution of colloidal silica is in said nonviscousphase, and directing said solution of colloidal silica into the fastflow paths whereupon said solution of colloidal silica reaches saidsolid gel phase in the fast flow paths thereby blocking flow of fluid inthe fast flow paths.
 2. The method of blocking flow in fast flow pathsin a geological formation of claim 1 wherein said step of preparing asolution of colloidal silica having a nonviscous phase and a solid gelphase includes preparing a solution of colloidal silica having anonviscous phase with a predetermined incubation period.
 3. The methodof blocking flow in fast flow paths in a geological formation of claim 2wherein said predetermined incubation period is predetermined byadjusting the silica content, colloid size, salinity, and pH, orpredetermined combinations of silica content, colloid size, salinity,and pH.
 4. The method of blocking flow in fast flow paths in ageological formation of claim 2 further comprising using reservoirmodeling and tracer test results in said step of allowing said solutionof colloidal silica to flow into the fast paths and reach said solid gelphase thereby blocking the flow of the fluid in the fast paths anddiverting the flow of the fluid into the other paths.
 5. A method ofimproving efficiency of production from underground formations whereinthe underground formations have fast paths for flow of production fluidand other paths for flow of the production fluid, comprising the stepsof: preparing a solution of colloidal silica having a nonviscous phaseand a solid gel phase, injecting said solution of colloidal silica intothe underground formations while said solution of colloidal silica is insaid nonviscous phase, and allowing said solution of colloidal silica toflow into the fast paths and reach said solid gel phase thereby blockingthe flow of the production fluid in the fast paths and diverting theflow of the production fluid into the other paths.
 6. The method ofimproving efficiency of production from underground formations of claim5 wherein said step of preparing a solution of colloidal silica having anonviscous phase and a solid gel phase includes preparing a solution ofcolloidal silica having a nonviscous phase with a predeterminedincubation period.
 7. The method of improving efficiency of productionfrom underground formations of claim 6 wherein said predeterminedincubation period is predetermined by adjusting the silica content,colloid size, salinity, and pH, or predetermined combinations of silicacontent, colloid size, salinity, and pH.
 8. The method of improvingefficiency of production from underground formations of claim 6 furthercomprising using reservoir modeling and tracer test results in said stepof allowing said solution of colloidal silica to flow into the fastpaths and reach said solid gel phase thereby blocking the flow of theproduction fluid in the fast paths and diverting the flow of theproduction fluid into the other paths.
 9. A method of improvingefficiency of production from a geothermal formation wherein thegeothermal formation has fast paths for flow of geothermal fluid andother paths for flow of the geothermal fluid, comprising the steps of:preparing a solution of colloidal silica having a nonviscous phase and asolid gel phase, injecting said solution of colloidal silica into thegeothermal formation while said solution of colloidal silica is in saidnonviscous phase, allowing said solution of colloidal silica to flowinto the fast paths and reach said solid gel phase thereby blocking theflow of the geothermal fluid in the fast paths and diverting the flow ofthe geothermal fluid into the other paths.
 10. The method of improvingefficiency of production from a geothermal formation of claim 9 whereinsaid step of preparing a solution of colloidal silica having anonviscous phase and a solid gel phase includes preparing a solution ofcolloidal silica having a nonviscous phase with a predeterminedincubation period.
 11. The method of improving efficiency of productionfrom a geothermal formation of claim 10 wherein said predeterminedincubation period is predetermined by adjusting the silica content,colloid size, salinity, and pH, or predetermined combinations of silicacontent, colloid size, salinity, and pH.
 12. The method of improvingefficiency of production from a geothermal formation of claim 10 furthercomprising using reservoir modeling and tracer test results in said stepof allowing said solution of colloidal silica to flow into the fastpaths and reach said solid gel phase thereby blocking the flow of thegeothermal fluid in the fast paths and diverting the flow of thegeothermal fluid into the other paths.
 13. A method of improvingefficiency of production from a primary geothermal formation usingcolloidal silica as a cementing agent to preferentially reducepermeability in zones proximate the primary geothermal formation,comprising the steps of: preparing a solution of colloidal silica havinga nonviscous phase and a solid gel phase, injecting said solution ofcolloidal silica into the zones proximate the primary geothermalformation while said solution of colloidal silica is in said nonviscousphase, allowing said solution of colloidal silica to flow into the zonesproximate the primary geothermal formation thereby blocking the zonesproximate the primary geothermal formation and improving efficiency ofproduction from the primary geothermal formation.
 14. The method ofimproving efficiency of production from a primary geothermal formationusing colloidal silica as a cementing agent to preferentially reducepermeability in zones proximate the primary geothermal formation ofclaim 13 wherein said step of preparing a solution of colloidal silicahaving a nonviscous phase and a solid gel phase includes preparing asolution of colloidal silica having a nonviscous phase with apredetermined incubation period.
 15. The method of improving efficiencyof production from a primary geothermal formation using colloidal silicaas a cementing agent to preferentially reduce permeability in zonesproximate the primary geothermal formation of claim 14 wherein saidpredetermined incubation period is predetermined by adjusting the silicacontent, colloid size, salinity, and pH, or predetermined combinationsof silica content, colloid size, salinity, and pH.
 16. A method ofimproving efficiency of production from an oil bearing formation,comprising the steps of: preparing a solution of colloidal silica havinga nonviscous phase and a solid gel phase, injecting said solution ofcolloidal silica into the oil bearing formation while said solution ofcolloidal silica is in said nonviscous phase, allowing said solution ofcolloidal silica to flow into the oil bearing formation therebyimproving efficiency of production from the oil bearing formation. 17.The method of improving efficiency of production from an oil bearingformation of claim 16 wherein said step of preparing a solution ofcolloidal silica having a nonviscous phase and a solid gel phaseincludes preparing a solution of colloidal silica having a nonviscousphase with a predetermined incubation period.
 18. The method ofimproving efficiency of production from an oil bearing formation ofclaim 17 wherein said predetermined incubation period is predeterminedby adjusting the silica content, colloid size, salinity, and pH, orpredetermined combinations of silica content, colloid size, salinity,and pH.